JPS6358200B2 - - Google Patents

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Publication number
JPS6358200B2
JPS6358200B2 JP1086180A JP1086180A JPS6358200B2 JP S6358200 B2 JPS6358200 B2 JP S6358200B2 JP 1086180 A JP1086180 A JP 1086180A JP 1086180 A JP1086180 A JP 1086180A JP S6358200 B2 JPS6358200 B2 JP S6358200B2
Authority
JP
Japan
Prior art keywords
acid
rolling
parts
compound
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1086180A
Other languages
Japanese (ja)
Other versions
JPS56109297A (en
Inventor
Koji Onoda
Yukio Hashiguchi
Takeo Yahiro
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Myoshi Oil and Fat Co Ltd
Original Assignee
Myoshi Oil and Fat Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Myoshi Oil and Fat Co Ltd filed Critical Myoshi Oil and Fat Co Ltd
Priority to JP1086180A priority Critical patent/JPS56109297A/en
Publication of JPS56109297A publication Critical patent/JPS56109297A/en
Publication of JPS6358200B2 publication Critical patent/JPS6358200B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、金属圧延油に関するものである。 従来圧延油として、鋼板用にはパーム油が古く
から使われ、それに代つて牛脂、豚脂、長須鯨硬
化油などの動植物油脂や鉱物油または、それらの
混合油をベースとして、それに添加剤、油性向上
剤、酸化防止剤、界面活性剤などを配合したもの
が広く使われている。 一方、圧延機械設備の進歩は著しく進み、ミル
の大型化に伴い、パス回数の削減、圧延速度の高
速化、圧延製品の規格精度の上昇等の圧延工程の
合理化並びに精密化が要求され、それに伴い圧延
油にかかる条件も苛酷なものとなつて来ており、
パーム油や牛脂系圧延油では、最早この条件を満
足し得ないものとなりつつあるが未だこれに代る
圧延油が見出されていないのが現状である。 本発明は従来のパーム油や牛脂系の圧延油より
すぐれた圧延性能を有し、現在要求されている苛
酷な圧延工程に対して、満足し得る圧延油を提供
せんとするものである。 本発明の圧延油は次のものにより構成される。 炭素数12〜22の脂肪族カルボン酸とポリアミン
を反応せしめて得られる1分子中に少なくとも1
個の活性水素を残存せしめたるアマイド化合物
に、さらにアルキレンオキシドを付加して得られ
る化合物(以下、AO付加物と略記す)と、ジカ
ルボン酸とを反応して得られる化合物を用いるこ
とを特徴とする金属圧延油であり、必要に応じ
て、極圧添加剤、界面活性剤、酸化防止剤等を配
合して用いることも可能である。 本発明に用いる炭素数12〜22の脂肪族カルボン
酸としては、ラウリン酸、ミリスチン酸、パルミ
チン酸、ステアリン酸、アラキン酸、ベヘン酸等
の飽和脂肪酸、オレイン酸、リノール酸、リノレ
ン酸、リシノール酸、アラキドン酸等の不飽和脂
肪酸が挙げられる。 次に炭素数12〜22の脂肪族カルボン酸と、ポリ
アミンとを反応して分子中に少なくとも1ケのア
ミン基を残存するアマイド化合物を得るが、ここ
に用いるポリアミンとしてはエチレンジアミン、
プロピレンジアミン、ヘキサメチレンジアミン、
ジエチレントリアミン、トリエチレンテトラミ
ン、テトラエチレンペンタミン、ペワタエチレン
ヘキサミンが挙げられる。 上記のアマイド化合物は、ポリアミンと炭素数
12〜22の脂肪族カルボン酸との間でアマイド化反
応を行つて得られる。その反応条件の一例を示せ
ば、ポリアミン1モルに対し、その分子中のアミ
ン基を少なくとも1ケ残存するように、脂肪族カ
ルボン酸のモル数を求め反応に用いる 例えば、エチレンジアミン1モルに対し、ラウ
リン酸ならば1モルを加え、窒素ガス気流下に
140〜260℃の温度で2〜25時間反応して目的のア
マイド化合物を得る。アマイド化合物分子中に残
存するアミン基の数はアミン価より算出する。 次にこのアマイド化合物にアルキレンオキシド
を付加してAO付加物を得る。このアマイド化合
物へのアルキレンオキシドの付加反応も常法によ
り行なわれる。ここで用いられるアルキレンオキ
シドとしては、エチレンオキシド、プロピレンオ
キシドが挙げられ、これらアルキレンオキシドは
1種のみを付加しても、また2種をランダムまた
はブロツク的に付加しても良く、その付加モル数
は2〜100モル、好ましくは3〜60モルである。 以上のようにして得られるAO付加物に、ジカ
ルボン酸を反応して本発明の金属圧延油に用いる
化合物を得る。AO付加物とジカルボン酸との反
応はAO付加物1モルにジカルボン酸0.3〜2モル
を加え、130〜200℃で反応して得られる。 本発明におけるジカルボン酸には、コハク酸、
アジピン酸、アゼライン酸、セバシン酸、マレイ
ン酸が挙げられる。 得られた反応生成物にアミンが残留する場合に
は必要に応じて、中和、四級化、両性化等の一般
的に知られている処理を、各々の処理に適した処
理剤を用いて行なつたのち、用いることができ
る。 これらの処理を行なうことによつて、反応生成
物の親水性を使用条件に応じて適正に調整するこ
とができるとともに、反応生成物の極性を調整
し、金属面への吸着性をコントロールすることも
できる。 これらの反応生成物はそのまま用いて、圧延油
として高い性能を有するが、従来の圧延油と混合
して使用することもでき、又必要に応じて極圧添
加剤、界面活性剤、酸化防止剤等を配合して用い
ることもできる。 以下実施例を挙げ本発明を更に詳細に説明す
る。 合成例 1 ベヘン酸684部、トリエチレンテトラミン146部
を窒素ガス気流下200〜240℃で20時間反応した
後、エチレンオキシド880部を160〜180℃で付加
反応して、酸価4.8、水酸基価64の化合物を得た。
次いでセバシン酸172部を加え、200〜220℃で10
時間反応し、酸価7.0、水酸基価7.4の化合物を得
た。 合成例 2 エチレンジアミン60部、ラウリン酸200部を窒
素ガス気流下150〜160℃で8時間反応した後、エ
チレンオキシド440部を140〜150℃で付加反応し
て、酸価1.8、水酸基価160.5の化合物を得た。次
いで、これにコハク酸118部を加え、180〜200℃
で8時間反応し、酸価10.2、水酸基価12.1の化合
物を得た。 合成例 3 ジエチレントリアミン103部、ステアリン酸568
部を窒素ガス気流下220〜240℃で8時間反応した
後、エチレンオキシド220部を160〜180℃で付加
反応し、次いでプロピレンオキシド174部を170〜
190℃で付加反応して、酸価1.2、水酸基価79.5の
化合物を得た。次いで、これにアゼライン酸146
部を加え、220〜250℃で16時間反応し、酸価
16.0、水酸基価12.0の化合物を得た。 合成例 4 ヘキサメチレンジアミン116部、オレイン酸282
部を窒素ガス気流下180〜190℃で10時間反応した
後、プロピレンオキシド870部を170〜180℃で付
加反応して、酸価1.5、水酸基価85.0の化合物を
得た。次いで、これにアジピン酸146部を加え、
180〜200℃で8時間反応し、酸価5.7、水酸基価
10.3の化合物を得た。 合成例 5 ペンタエチレンヘキサミン232部、リシノール
酸894部を窒素ガス気流下190〜200℃で8時間反
応した後、エチレンオキシド880部を160〜170℃
で付加反応し、次いでプロピレンオキシド580部
を180〜190℃で付加反応して、酸価1.5、水酸基
価132.0の化合物を得た。次いで、これに無水マ
レイン酸98部を加え、180〜200℃で8時間反応
し、酸価5.2、水酸基価80.0の化合物を得た。 合成例1〜5で得た化合物を用いた表−1に示
す組成の圧延油の実施例1〜5の摩擦係数(μ)、
耐圧性の測定を行い、その結果を比較例として牛
脂系圧延油の測定結果とともに表−2に示した。
また、圧延性能試験は実施例1〜3については圧
延材料に一定量の圧延油をそのまま塗布し、また
実施例4,5および比較例については5%濃度の
エマルジヨンとして供給して試験を行つた。圧延
材料への付着油量は、実施例1〜5及び比較例の
すべて1g/m2となるようにした。 試験の結果を圧下率(%)と圧延荷重(ton)
との関係をもつて圧延性能評価とし、図−1に示
した。 本発明の圧延油の潤滑性能に関する試験方法は
次の通りである。 摩擦係数(μ)試験法 曽田式振り子型油性試験機N型 耐荷重能試験法 シエル型高速四球式摩擦試験機
The present invention relates to metal rolling oil. Conventionally, palm oil has been used as a rolling oil for steel plates for a long time, but instead, animal and vegetable oils such as beef tallow, lard, Nagasu whale hardened oil, mineral oils, or mixtures of these oils are used as base oils, and additives and oil-based oils are used as rolling oils. Products containing improvers, antioxidants, surfactants, etc. are widely used. On the other hand, the progress of rolling machinery equipment has progressed significantly, and as mills have become larger, there has been a demand for rationalization and precision of the rolling process, such as reducing the number of passes, increasing rolling speed, and increasing the standard accuracy of rolled products. As a result, the conditions for rolling oil are becoming more severe.
Palm oil and tallow-based rolling oils are no longer able to satisfy this condition, but at present no alternative rolling oil has yet been found. The present invention aims to provide a rolling oil that has better rolling performance than conventional palm oil or beef tallow-based rolling oils and can satisfy the harsh rolling processes currently required. The rolling oil of the present invention is composed of the following. At least 1 in 1 molecule obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with a polyamine.
It is characterized by using a compound obtained by reacting a compound obtained by further adding an alkylene oxide (hereinafter abbreviated as AO adduct) with a dicarboxylic acid to an amide compound in which active hydrogens remain. It is a metal rolling oil that can be used by adding extreme pressure additives, surfactants, antioxidants, etc. as necessary. The aliphatic carboxylic acids having 12 to 22 carbon atoms used in the present invention include saturated fatty acids such as lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, and behenic acid, oleic acid, linoleic acid, linolenic acid, and ricinoleic acid. and unsaturated fatty acids such as arachidonic acid. Next, an aliphatic carboxylic acid having 12 to 22 carbon atoms is reacted with a polyamine to obtain an amide compound in which at least one amine group remains in the molecule.The polyamine used here is ethylenediamine,
propylene diamine, hexamethylene diamine,
Examples include diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and pewataethylenehexamine. The above amide compound has a polyamine and a carbon number
It is obtained by performing an amide reaction with 12 to 22 aliphatic carboxylic acids. To give an example of the reaction conditions, the number of moles of aliphatic carboxylic acid used in the reaction is determined so that at least one amine group remains in the molecule for 1 mole of polyamine. For example, for 1 mole of ethylenediamine, For lauric acid, add 1 mole and place under nitrogen gas flow.
The desired amide compound is obtained by reacting at a temperature of 140 to 260°C for 2 to 25 hours. The number of amine groups remaining in the amide compound molecule is calculated from the amine value. Next, an alkylene oxide is added to this amide compound to obtain an AO adduct. The addition reaction of alkylene oxide to this amide compound is also carried out by a conventional method. Examples of the alkylene oxide used here include ethylene oxide and propylene oxide, and these alkylene oxides may be added alone or in a random or block manner, and the number of moles added is The amount is from 2 to 100 mol, preferably from 3 to 60 mol. The AO adduct obtained as described above is reacted with a dicarboxylic acid to obtain a compound used in the metal rolling oil of the present invention. The reaction between the AO adduct and dicarboxylic acid is obtained by adding 0.3 to 2 moles of dicarboxylic acid to 1 mole of the AO adduct and reacting at 130 to 200°C. Dicarboxylic acids in the present invention include succinic acid,
Examples include adipic acid, azelaic acid, sebacic acid, and maleic acid. If amines remain in the resulting reaction product, generally known treatments such as neutralization, quaternization, and amphotericization may be performed as necessary using processing agents suitable for each treatment. After doing so, it can be used. By performing these treatments, it is possible to appropriately adjust the hydrophilicity of the reaction product according to the usage conditions, and also to adjust the polarity of the reaction product and control its adsorption to metal surfaces. You can also do it. These reaction products have high performance as rolling oil when used as is, but they can also be used by mixing with conventional rolling oil, and if necessary, extreme pressure additives, surfactants, and antioxidants may be added. It is also possible to use a mixture of the following. The present invention will be explained in more detail with reference to Examples below. Synthesis Example 1 After reacting 684 parts of behenic acid and 146 parts of triethylenetetramine at 200 to 240°C under a nitrogen gas stream for 20 hours, addition reaction with 880 parts of ethylene oxide at 160 to 180°C resulted in an acid value of 4.8 and a hydroxyl value of 64. The compound was obtained.
Next, 172 parts of sebacic acid was added and heated at 200 to 220°C for 10 minutes.
The reaction was carried out for a period of time to obtain a compound with an acid value of 7.0 and a hydroxyl value of 7.4. Synthesis Example 2 After reacting 60 parts of ethylenediamine and 200 parts of lauric acid at 150 to 160°C under a nitrogen gas stream for 8 hours, addition reaction of 440 parts of ethylene oxide was carried out at 140 to 150°C to obtain a compound with an acid value of 1.8 and a hydroxyl value of 160.5. I got it. Next, add 118 parts of succinic acid to this and heat at 180-200℃.
The mixture was reacted for 8 hours to obtain a compound with an acid value of 10.2 and a hydroxyl value of 12.1. Synthesis example 3 103 parts of diethylenetriamine, 568 parts of stearic acid
After reacting for 8 hours at 220-240°C under a nitrogen gas stream, 220 parts of ethylene oxide was added at 160-180°C, and then 174 parts of propylene oxide was added at 170-240°C.
An addition reaction was carried out at 190°C to obtain a compound with an acid value of 1.2 and a hydroxyl value of 79.5. This is then added to azelaic acid 146
of the acid value and reacted at 220-250℃ for 16 hours.
16.0, and a compound with a hydroxyl value of 12.0 was obtained. Synthesis example 4 116 parts of hexamethylene diamine, 282 parts of oleic acid
After reacting for 10 hours at 180 to 190°C under a nitrogen gas stream, 870 parts of propylene oxide was subjected to an addition reaction at 170 to 180°C to obtain a compound having an acid value of 1.5 and a hydroxyl value of 85.0. Next, 146 parts of adipic acid was added to this,
Reacted at 180-200℃ for 8 hours, acid value 5.7, hydroxyl value
Compound 10.3 was obtained. Synthesis Example 5 After reacting 232 parts of pentaethylenehexamine and 894 parts of ricinoleic acid at 190 to 200°C under a nitrogen gas stream for 8 hours, 880 parts of ethylene oxide was reacted at 160 to 170°C.
Then, 580 parts of propylene oxide was added thereto at 180 to 190°C to obtain a compound having an acid value of 1.5 and a hydroxyl value of 132.0. Next, 98 parts of maleic anhydride was added thereto, and the mixture was reacted at 180 to 200°C for 8 hours to obtain a compound having an acid value of 5.2 and a hydroxyl value of 80.0. Friction coefficient (μ) of Examples 1 to 5 of rolling oil having the composition shown in Table 1 using the compounds obtained in Synthesis Examples 1 to 5,
The pressure resistance was measured, and the results are shown in Table 2 as a comparative example along with the measurement results of tallow-based rolling oil.
In addition, rolling performance tests were conducted by applying a certain amount of rolling oil to the rolled material as it was for Examples 1 to 3, and by supplying it as a 5% concentration emulsion for Examples 4 and 5 and Comparative Examples. . The amount of oil adhering to the rolled material was 1 g/m 2 in all Examples 1 to 5 and Comparative Example. Test results are shown in rolling reduction ratio (%) and rolling load (ton)
The relationship between rolling performance and rolling performance is evaluated and shown in Figure 1. The test method regarding the lubrication performance of the rolling oil of the present invention is as follows. Friction coefficient (μ) test method Soda pendulum type oil tester N type load-bearing capacity test method Shell type high speed four-ball friction tester

【表】【table】

【表】 圧延試験法 圧延機:四段ロール式圧延機 ワークロール径150mm×巾140mm バツクアツプロール径250mm×巾140mm ロール材質 クロム鋼 ロール周速30m/min 圧延材料:SPC―C 厚さ0.6mm×巾50mm×長さ150mm 圧延性能の測定法 圧延前の鋼板に50mmの間隔(l1)の2本
の線を引き、これを圧延して圧延後の間
隔(l2)を測定し、次式により圧下率を
求めた。 圧下率(%)=l2−l1/l2×100 またその時の圧延荷重(ton)をロー
ドセルにて測定した。
[Table] Rolling test method Rolling machine: Four-high roll rolling machine Work roll diameter 150 mm x width 140 mm Back-up roll diameter 250 mm x width 140 mm Roll material Chrome steel roll circumferential speed 30 m/min Rolling material: SPC-C Thickness 0.6 mm × Width 50 mm × Length 150 mm Method of measuring rolling performance Two lines with a spacing of 50 mm (l 1 ) are drawn on the steel plate before rolling, the lines are rolled, and the spacing after rolling (l 2 ) is measured. The rolling reduction ratio was calculated using the formula. Rolling ratio (%)=l 2 −l 1 /l 2 ×100 Further, the rolling load (ton) at that time was measured using a load cell.

【図面の簡単な説明】[Brief explanation of the drawing]

図1は、本発明圧延油実施例1〜5と、比較例
の圧延性能を圧延荷重と圧下率の関係により示し
た圧延性能比較線図である。
FIG. 1 is a rolling performance comparison diagram showing the rolling performance of Examples 1 to 5 of the rolling oil of the present invention and a comparative example based on the relationship between rolling load and rolling reduction.

Claims (1)

【特許請求の範囲】[Claims] 1 炭素数12〜22の脂肪族カルボン酸と、ポリア
ミンを反応せしめて得られる、1分子中に少なく
とも1個の活性水素を残存せしめたるアマイド化
合物にさらにアルキレンオキシドを付加して得ら
れる化合物と、ジカルボン酸とを反応して得られ
る化合物を用いることを特徴とする金属圧延油。
1. A compound obtained by further adding an alkylene oxide to an amide compound in which at least one active hydrogen remains in one molecule, which is obtained by reacting an aliphatic carboxylic acid having 12 to 22 carbon atoms with a polyamine; A metal rolling oil characterized by using a compound obtained by reacting with a dicarboxylic acid.
JP1086180A 1980-02-02 1980-02-02 Metal rolling oil Granted JPS56109297A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1086180A JPS56109297A (en) 1980-02-02 1980-02-02 Metal rolling oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1086180A JPS56109297A (en) 1980-02-02 1980-02-02 Metal rolling oil

Related Child Applications (2)

Application Number Title Priority Date Filing Date
JP1387387A Division JPS6339987A (en) 1987-01-23 1987-01-23 Metal rolling oil
JP1387487A Division JPS6339988A (en) 1987-01-23 1987-01-23 Metal rolling oil

Publications (2)

Publication Number Publication Date
JPS56109297A JPS56109297A (en) 1981-08-29
JPS6358200B2 true JPS6358200B2 (en) 1988-11-15

Family

ID=11762129

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1086180A Granted JPS56109297A (en) 1980-02-02 1980-02-02 Metal rolling oil

Country Status (1)

Country Link
JP (1) JPS56109297A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01311193A (en) * 1988-06-08 1989-12-15 Dai Ichi Kogyo Seiyaku Co Ltd Additive for metal cold rolling oil
JPH07119429B2 (en) * 1989-11-10 1995-12-20 共栄社化学株式会社 Method for producing high softening point wax

Also Published As

Publication number Publication date
JPS56109297A (en) 1981-08-29

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